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The calculation of the critical locus curve of a binary hydrocarbon system
Author(s) -
Hissong Douglas W.,
Kay Webster B.
Publication year - 1970
Publication title -
aiche journal
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.958
H-Index - 167
eISSN - 1547-5905
pISSN - 0001-1541
DOI - 10.1002/aic.690160413
Subject(s) - binary number , critical point (mathematics) , hydrocarbon mixtures , thermodynamics , binary system , equation of state , hydrocarbon , component (thermodynamics) , reduced properties , mathematics , statistical physics , chemistry , mathematical analysis , physics , arithmetic , organic chemistry
A method of calculating the critical properties of binary hydrocarbon systems is presented which is based upon the rigorous thermodynamic equations for the critical point of a binary mixture. By using these equations together with an equation of state, a completely analytical procedure was developed with the aid of a digital computer. The Redlich‐Kwong and the Dieterici equations of state were chosen for study. The Redlich‐Kwong equation was found superior for predicting critical pressures and temperatures by this method, although the Dieterici equation was better for critical volumes. The two interaction parameters arising from the equation of state were calculated from combining rules or from available experimental critical data on binary systems. To facilitate the latter approach, a mathematical optimization routine was used to find the best values of the interaction parameters for twenty‐one binary hydrocarbon systems for which critical data were experimentally determined. The optimum values of the interaction parameters were correlated as functions of the ratio of molecular weights of the components. These correlations enable one to predict quite precisely the critical properties of the binary systems from the pure component data alone.